CN101392032B - Method for preparing bamboo leaf polysaccharide extract by member separation - Google Patents
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Abstract
The invention discloses a membrane separation method for preparing bamboo leaf polysaccharide extracts, which comprises the following steps: firstly, a lipophilic solvent is used for extracting screened bamboo leaves; secondly, aliphatic alcohol or acetone of C1-C3 is used for extracting the remained bamboo leaf slags; then, deionized water purified by a reverse osmose membrane is used for extracting remained bamboo leaf slags; thirdly, alkalic centrifugal settling is carried out to obtain a centrifugal clear solution and sediments; the centrifugal clear solution goes through the treatment of a ceramic membrane, an ultrafiltration membrane and a nanofiltration membrane sequentially, thus obtaining concentrated solution going through the nanofiltration membrane; the concentrated solution going through the nanofiltration membrane is adsorbed by a decolorizing resin; the polysaccharide solution is concentrated under vacuum until the ratio thereof is 1.03 to 1.14; the aliphatic alcohol of C1-C3 is used for settling the polysaccharide, and settlements are centrifuged and dried by microwave under vacuum; the solid part is dried by microwave under vacuum to obtain the bamboo leaf polysaccharide extracts with high-content polysaccharide.
Description
Technical field
The present invention relates to a kind of separation method of leaf of bamboo polysaccharide, particularly a kind of membrane sepn prepares the method for high purity leaf of bamboo polysaccharide.
Background technology
Along with the raising of people's living standard, back to nature, natural health food, the notion of green food is more and more goed deep into people's life idea, and whole food and medicine have become the trend and the fashion of international food and drug development.Folium Bambosae extract just constantly is familiar with by people as a kind of extract natural, that have different physiological roles.
Bamboo is a class plant that belongs to Gramineae Bambusoideae (Bambusadea), and the whole world has 70 to belong to 1225 kinds approximately.46 ° of the north latitude that bamboo plant is distributed in the earth are to the torrid zone between 47 ° in the south latitude, subtropics and area, warm temperate zone, the main island that are distributed in Asia, Africa, South and North America, the Oceanian torrid zone, subtropical zone and corresponding position, the Pacific Ocean of concentrating, the torrid zone in South East Asia, subtropics are its center of distribution area.The bamboo grove area increases with annual 3% speed, how rationally efficiently to utilize bamboo resource, promotes the development of bamboo industry, has become problem of showing great attention in world's production of forestry.China is one of producing region, bamboo center, accounts for 25% of world's bamboo grove total area.Development and use bamboo class forest reserves meaning is very great.The leaf of bamboo has long edible and medicinal history in China, and the leaf of bamboo is light, little puckery, cold, and it is sweet, bitter to distinguish the flavor of, and it is thirsty to cure mainly dysphoria with smothery sensation, fever of children, infantile malnutrition, pyreticosis egersis, ulceration on the oral mucosa and the tongue, conjunctival congestion with pain and swelling of the eye, mange, sore, pharyngolaryngitis, diseases such as traumatic hemorrhage.Contain effective constituents such as a large amount of flavonoid compounds and bioactive polysaccharide in the leaf of bamboo, leaf of bamboo active polysaccharide by raise immunity, promote the generation of immune factor and activate and realize antitumor action to have multiple efficacies such as good immunomodulatory, antitumor, anti-infective, anti-inflammatory.Be subjected at present the extensive concern of domestic and international market.The Japanese also gets a kind of active polysaccharide from the indicalamus leaf extraction separation, through evidence S-180 is had good restraining and removes effect.
At present both at home and abroad seldom, for the method report that prepare high-content leaf of bamboo polysaccharide especially polysaccharide content greater than 80% leaf of bamboo polyoses extract.
Summary of the invention
For the lower defective of content of leaf of bamboo polysaccharide in the leaf of bamboo polyoses extract that solves the prior art existence, the invention provides a kind of method of preparing bamboo leaf polysaccharide extract by member separation, can make the leaf of bamboo polyoses extract that polysaccharide content is higher than 80%wt.
The present invention adopts following technical scheme: a kind of method of preparing bamboo leaf polysaccharide extract by member separation may further comprise the steps:
The first step is extracted the leaf of bamboo polysaccharide content that the filters out leaf of bamboo greater than 5.0%wt with lipophilic solvent earlier, and wherein the mass ratio of lipophilic solvent and the leaf of bamboo is (1-30): 1, and the extraction temperature is 20 ℃-100 ℃, extraction time is 0.5h-72h; Extracting mode can be selected any one or its combination in thermal backflow extraction, microwave extraction, the ultrasonic extraction.80 ℃-100 ℃ of temperature are extracted in thermal backflow, and the time is 0.5-10 hour; Microwave extraction power 100-2000W, time 10-120 minute, 50 ℃-70 ℃ of temperature; Ultrasonic extraction power 300W-3KW, time 10-120 minute, 50 ℃-70 ℃ of temperature.Leaf of bamboo polysaccharide content greater than the screening method of the leaf of bamboo of 5.0%wt is: with sulfuric acid-anthrone method, with glucose as a standard, set up the glucose typical curve, product with glucose as a standard then, under the 610nm leaf of bamboo of collecting is carried out colorimetric estimation leaf of bamboo polysaccharide content, filter out the leaf of bamboo of leaf of bamboo polysaccharide content greater than 5.0%wt.The leaf of bamboo of goose feather bamboo, floor file bamboo, mao bamboon, Tang Zhu or the spun gold cizu bottom in preferred Nanjing, the perhaps leaf of bamboo of Chizhou City, Anhui mao bamboon.Lipophilic solvent is C
5-C
7Fat alkane or the sherwood oil of 60 ℃-120 ℃ of boiling ranges.Described C
5-C
7Fat alkane be in Skellysolve A, normal hexane or the normal heptane any one.
In second step, use C again
1-C
3Fatty Alcohol(C12-C14 and C12-C18) or acetone to be extraction agent extract the leaf of bamboo residue of the first step, the mass ratio of the extraction agent and the leaf of bamboo is (1-20): 1, extracting temperature is 20 ℃-100 ℃, extraction time is 0.5h-72h; C
1-C
3Fatty Alcohol(C12-C14 and C12-C18) be in methyl alcohol, ethanol, the n-propyl alcohol any one.
In the 3rd step, with the deionized water extraction leaf of bamboo residue in second step, the mass ratio of the deionized water and the leaf of bamboo is (1-20): 1, and extracting temperature is 80 ℃-110 ℃, extraction time is 0.5h-5h;
The 4th step, centrifugal settling: the extracting solution of the 3rd step deionized water is regulated pH to 8-9,, obtain centrifugal clear liquid and throw out with the centrifugal settling of 6000-20000r/min speed;
The 5th step, the film lotus root is closed separation: the centrifugal clear liquid that the 4th step was obtained obtains concentrated solution at last by ceramic membrane, ultra-filtration membrane and nanofiltration membrane treatment successively, wherein, the ceramic membrane mean pore size is 0.1-0.5 μ m, the ultra-filtration membrane molecular weight cut-off is 5000-200000 dalton, nanofiltration membrane molecular weight cut-off 200-1000 dalton, material is by ultra-filtration membrane and nanofiltration membrane flux 1-10m
3/ m
2HMpa;
The 6th step, decolouring, the concentrated solution that the 5th step was obtained adsorbs by decolorizing resin, and the ratio of the volume of the quality of the resin of adding and the concentrated solution of adding is 1-50:100, and churning time is 5-60min, 5 ℃-80 ℃ of temperature; Decolorizing resin refers among D845, D941, D280, D392, D291, D730, D293, the D296 any one.
In the 7th step, alcohol is analysed, and the 6th leaf of bamboo polysaccharide soln of step after the resin decolorization is vacuumized to be concentrated into proportion be 1.03-1.14, as proportion 1.12, adds C
1-C
3Fatty Alcohol(C12-C14 and C12-C18) stir, Fatty Alcohol(C12-C14 and C12-C18) and polysaccharide soln volume ratio are 4-20:1, obtain throw out with the filtration of 160 order filter clothes again;
The 8th step, vacuum-drying, the throw out that the 7th step obtained is centrifugal, with the centrifugal settling of 3000-10000r/min speed, obtain centrifugal solids and partly use the 600-2000W microwave vacuum drying, 25 ℃-60 ℃ of temperature, vacuum tightness 250-700mmHg obtains the leaf of bamboo polyoses extract of leaf of bamboo polysaccharide content greater than 80%wt.
The present invention obtains following technique effect:
1. by the contained leaf of bamboo polysaccharide content of 30 kinds of leaf of bamboves of different places of production different sites is analyzed, filter out the kind of high-content leaf of bamboo polysaccharide, help the preparation of high-content leaf of bamboo polysaccharide.
2. according to the similar principle that mixes, adopt the polarity solvent to extract successively, remove impurity such as lipoclastic, pigment, alcohol soluble substance as far as possible, improved leaf of bamboo polysaccharide concentration in the deionized water extraction thing, also help the use of protective membrane equipment.
3. adopt dissimilar membrane sepn lotus roots to close technology first and decolouring absorption lotus root is closed technology generation for traditional solvent extration, the content that can not only make leaf of bamboo polysaccharide in the leaf of bamboo polyoses extract is greater than 80%wt, and saves the energy, clean environment firendly.
4. adopt pH sedimentation centrifuging purifying first, can not only remove impurity such as macromolecule protein, colloid, chlorophyll, polymer tannin, improve the purity of leaf of bamboo polyoses extract, and help protection and the regeneration that lotus root is closed membrane module, prolong its life-span.
5. select the decolouring polymeric adsorbent to replace the solvent extraction Deproteinization, both economized solvent, can effectively improve the content of leaf of bamboo polysaccharide again.
Description of drawings
Fig. 1 ceramic membrane current curve.
Fig. 2 ultra-filtration membrane current curve.
Embodiment
Leaf of bamboo polysaccharide content is as follows greater than the screening method of the leaf of bamboo of 5.0%wt:
(1), with glucose as a standard, sets up the glucose typical curve, as table 1 with sulfuric acid-anthrone method
Table 1 glucose typical curve
To the absorbance A linear regression, get regression equation A=5.8137C-0.00473 (R=0.9987) with glucose content C (mg).Show that glucose is the better linearity relation with absorbancy in 0.0 μ g/mL~96.0 μ g/mL scopes.
2) sample polysaccharide replication test
Get 4 parts of identical green bamboo leaf polyose extracting solutions respectively, the result such as the table 2 of replication leaf of bamboo polysaccharide.Test-results shows, product with glucose as a standard, and the method for colorimetric estimation leaf of bamboo polysaccharide is feasible under the 610nm, and better repeatability is arranged.
Table 2 polysaccharide determination replica test data
3) sample polysaccharide average recovery is measured
The leaf of bamboo polysaccharide sample size that adds in each group is 0.06mg/mL * 10mL=0.6mg, and the glucose standard substance of adding are respectively 0.12mg/mL * 4mL=0.48mg, 0.12mg/mL * 5mL=0.6mg, 0.12mg/mL * 6mL=0.72mg.The rate of recovery is respectively 101.92%, 101.68%, 99.89%, and standard deviation is 0.0110, meets the requirements, and has proved the reliability of this method.
Table 3 average recovery testing data
This patent is measured leaf of bamboo active polysaccharide components contents in 30 kind leaf of bamboves by setting up leaf of bamboo analysis of polysaccharide method.The result shows, by percentage to the quality: leaf of bamboo polysaccharide content is between 1.94%~7.69%, wherein leaf of bamboo polysaccharide content is having area, Nanjing leaflet indocalamus (4.59%) more than 4%, short indocalamus (4.82%), Bashan Mountain wood bamboo 4.43%, goose feather bamboo (7.69%), floor file bamboo (5.69%), mao bamboon (5.36%), hundred folder bamboos (4.86%), Tang Zhu (5.30%), spun gold cizu bottom (5.73%), Fujian Province Youxi green bamboo (4.36%), mao bamboon (4.72%), the goose feather bamboo in Chizhou City, Anhui (5.90%), especially Nanjing, the floor file bamboo, mao bamboon, Tang Zhu and spun gold cizu bottom, Chizhou City, Anhui mao bamboon distributes wide, polysaccharide content is higher than 5%, becomes the optimum feed stock of industrial extraction leaf of bamboo active polysaccharide component through the screening of this patent.Different with position leaf of bamboo polysaccharide content about the leaf of bamboo of kind, and content all is that bottom Lao Ye is higher than top tender leaf.Result such as table 4.
Polysaccharide content in the table 4 different varieties leaf of bamboo
As shown in Table 4, the content range of leaf of bamboo polysaccharide is, by percentage to the quality: 1.94%~7.69%, i.e. 19.4mg/g~76.9mg/g, by the height that contains polysaccharide, with its be divided into content more than 4%, between 3%~4%, between 2%~3%, four classes below 2%.
More than the 4%wt: area, Nanjing leaflet indocalamus (4.59%) is arranged, short indocalamus (4.82%), Bashan Mountain wood bamboo 4.43%, goose feather bamboo (7.69%), floor file bamboo (5.69%), mao bamboon (5.36%), hundred folder bamboos (4.86%), Tang Zhu (5.30%), spun gold cizu bottom (5.73%), Fujian Province Youxi green bamboo (4.36%), mao bamboon (4.72%), Chizhou City, Anhui (5.90%); Between 3%~4%: the beard indocalamus of Nan Linda, the spire indocalamus, under the bitter bamboo, the spire bitter bamboo, under the bitter bamboo that comes into leaves, beautiful bamboo, the bamboo of showing filal obedience, phyllostachys nigra var. henonis is on the spun gold cizu; Woodsization fishscale bamboo; Fujian Youxi bitter bamboo; The bitter bamboo of Chizhou City, Anhui; Between 2%~3%: the indocalamus of Nan Linda, broadleaf indocalamus is upper and lower, on the bitter bamboo, on the wood bamboo of the Bashan Mountain, henon bamboo; The henon bamboo of Fujian Youxi; Below 2%: on the bitter bamboo that comes into leaves of Nan Linda.
Different with the mao bamboon in the Nanjing bamboo plantation of kind, Youxi mao bamboon and Chizhou City's mao bamboon polysaccharide content, be respectively: 5.36%, 4.72%, 5.90%; The bitter bamboo content in three places is respectively, and: Nan Linda is last 2.81%, under the Nan Linda 3.21%, and Youxi 3.35%, Chizhou City 3.25%.Therefore, different with position polysaccharide content about the leaf of bamboo of kind, and content all is that bottom Lao Ye is higher than top tender leaf.Thereby polysaccharide to be enriched in the old blade in bottom.
The extracting mode explanation:
Extracting mode among the present invention in the first step can be selected a kind of in thermal backflow, microwave extraction, the ultrasonic extraction.80 ℃-100 ℃ of temperature are extracted in thermal backflow, and the time is 0.5-10 hour; Microwave extraction power 100-2000W, time 10-120 minute, 50 ℃-70 ℃ of temperature; Ultrasonic extraction power 300W-3KW, time 10-120 minute, 50 ℃-70 ℃ of temperature.
In the present invention program, before the polar solvent extraction, use earlier non-polar solvent, extract as the leaf of bamboo to screening such as sherwood oil, normal hexane, ether, mass ratio is (1-30): 1, and extracting temperature is 20 ℃-100 ℃, extraction time is 0.5h-72h, purpose is the weeding of grease solubility impurity, comprises pigments such as chlorophyll.Experiment is result repeatedly show, can remove the impurity of 1-3%wt.Use C again
1-C
3Fatty Alcohol(C12-C14 and C12-C18), as methyl alcohol, ethanol or acetone remaining leaf of bamboo residue is extracted, purpose is removed impurity such as the polyphenol, tannin, flavones, terpene, saponin(e, alkaloid of pure dissolubility, experiment result repeatedly shows, can remove the impurity of 5-15%wt.Prepare deionized water with reverse osmosis membrane, extract remaining leaf of bamboo residue, the mass ratio of the deionized water and the leaf of bamboo is (1-20): 1, and extracting temperature is 80 ℃-110 ℃, extraction time is 0.5h-5h; The polyose activeconstituents is water-soluble, and extraction yield is greater than 95%.
Press L among the present invention
9(3
4) orthogonal table adopts respectively that water is carried, ultrasonic wave lixiviate, microwave leach extraction method, and leaf of bamboo polysaccharide extracting process parameter is tested, and measures polysaccharide content with sulfuric acid one phynol method.
The design of the table 2 water extraction process factor
Table 3 L
9(3
4) water puies forward Orthogonal experiment results
The primary and secondary pass that influences leaf of bamboo polysaccharide extract rate factor is: extracting solid-to-liquid ratio polysaccharide extract rate is had the greatest impact, is extraction time secondly, and the influence of temperature and time is less relatively. its best lixiviate parameter is A
2B
3C
3D
3, promptly under 80 ℃, lixiviate 100min, solid-to-liquid ratio 1:25, lixiviate 3 times. under top condition, polysaccharide yield is 0.661%.
The design of the table 4 ultrasonic extracting process factor
Table 5 L
9(3
4) the ultrasonic extraction Orthogonal experiment results
From the watch test result as can be known, extraction time has the greatest impact to extraction yield, is temperature secondly, and time and solid-to-liquid ratio are less to the influence of extraction yield. and its best lixiviate parameter is A
3B
2C
1D
3, promptly under 70 ℃, lixiviate 20min, solid-to-liquid ratio 1:20, lixiviate 3 times, polysaccharide yield is 0.695%.Consider the cost problem of following process, the solid-to-liquid ratio of preferred 1:15, lixiviate 10min.
The design of the table 6 microwave-assisted extraction process factor
Table 7 L
9(3
4) microwave-assisted extraction Orthogonal experiment results
From the watch test result as can be known, microwave power and extraction time have the greatest impact to extraction effect, secondly are time and solid-to-liquid ratio. and its best lixiviate parameter is A
3B
2C
ID
3, promptly under the condition of microwave power 800W,, extract 10min by solid-to-liquid ratio 1:15, lixiviate 3 times, polysaccharide yield is 0.658%.
The result shows: the polysaccharide extract rate of microwave lixiviate 5-10min and water are carried quite, and the extraction yield of ultrasonic wave lixiviate is higher than water and carries and the microwave lixiviate.
With microwave and ultrasonic wave vat liquor, regulating pH with 0.5%-5% alkali lye is 8-9 among the present invention, has a large amount of precipitations to produce.Select 3000-10000 rev/min of whizzer centrifugal settling of rotating speed, add deionized water in the throw out, the mass ratio of throw out and deionized water is 1:1-10, preferred 1:4, and disgorging merges twice clear liquid.Adopt present method to handle and not only remove a large amount of insoluble solids, colloid, chlorophyll, high score, improve the content of polysaccharide in the extracting solution from impurity such as protein, and protective membrane assembly and decolorizing resin, help improving production effect.
In the present invention, adopt the film lotus root to close isolation technique, the clear liquid of centrifugal settling is attached together by ceramic membrane, ultra-filtration membrane and nanofiltration membrane lotus root successively put, obtain concentrated solution at last.The inorganic ceramic membrane material is an aluminium sesquioxide, mean pore size 0.1-0.5 μ m, it is the polysulfone membrane (PS) of 5000 ~ 200000 dalton (Dalton) that ultra-filtration membrane is selected molecular weight cut-off, preferred 100000-15000Dalton, nanofiltration membrane is truncated into stays molecular weight 200 ~ 1000Dalton polyimide film, and material is by ultra-filtration membrane and nanofiltration membrane flux 1-10m
3/ m
2HMpa.Compare with traditional vacuum rotary drum filter, diatomite filter, adopt the ceramic membrane filter technology, not only can remove impurity such as tiny insoluble solids, a large amount of polymer tannin, protein, colloid, fiber, bacterium and chlorophyll, and greatly reduce the pollution of subsequent ultrafiltration film, nanofiltration membrane and decolorizing resin, under certain pressure, when the material filtrate flow is crossed the film surface, only allow water and the small-molecule substance littler to pass through than membrane pore size, reach solution purification, separation, with spissated purpose, thereby improve the content of polysaccharide in the concentrated solution.As shown in table 8.
Table 8 polysaccharide content and rejection
Tab.6-2The?content?and?removal?of?polysaccharide
Fig. 1 extracts the film flow velocity that records when polysaccharide liquid is crossed ceramic membrane for pilot scale, and operational condition: extract concentration is 9.32g/L, and temperature is 30 ℃~40 ℃, and pressure is less than 0.2MPa.As can be seen, ceramic membrane flow velocity after 20 minutes is basicly stable.
Fig. 2 extracts the film flow velocity that records when polysaccharide liquid is crossed ultra-filtration membrane for pilot scale, and extract concentration is 7.08g/L, and temperature is 26.5 ℃, and pressure is 0.24MPa.As can be seen, ultra-filtration membrane flow velocity after 5 minutes is basicly stable.
Among the present invention, through inorganic ceramic film, 10Dalton ultra-filtration membrane and 200Dalton nanofiltration membrane treatment, the content of polysaccharide can reach 38.24% in the concentrated solution, and it is low to have improved in the Crude polysaccharides extract that traditional water extracting alcohol analysis method obtains polysaccharide content widely, the alcohol consumption is big, the problem that energy consumption is big.
The present invention adopts one or more media among macropore resinoid D845, D941, D280, D392, D291, D730, D293, the D296 etc., and to be filler carry out selective adsorption to the concentrated solution of nanofiltration membrane, and the concentrated solution volume of resin and nanofiltration membrane is than being 1:5-20.Preferred D845, D941, D280,, D392, greater than 85%, the rate of loss of polysaccharide is less than 10% to the percent of decolourization of polyoses extract for they.
Leaf of bamboo polysaccharide soln after macroporous resin is decoloured in the present invention vacuumizes and is concentrated into proportion is 1.03-1.14, and preferred specific gravity 1.10-1.12 adds 85% above C
1-C
3Fatty Alcohol(C12-C14 and C12-C18) stir, as methyl alcohol, ethanol etc., Fatty Alcohol(C12-C14 and C12-C18) and polysaccharide soln volume ratio are 420:1, preferred 4-6:1, purpose is with polysaccharide precipitation, obtains the polysaccharide precipitation thing with the filtration of 160 order filter clothes again; Pass through the centrifugal settling of 3000-10000r/min speed again, preferred 6000-10000r/min, obtain centrifugal solids and partly use the 600-2000W microwave vacuum drying, 25 ℃-60 ℃ of temperature, preferred 30 ℃-40 ℃, vacuum tightness 250-700mmHg obtains the leaf of bamboo polyoses extract of leaf of bamboo polysaccharide content greater than 80%wt.
The screening method of embodiment 1 high-content leaf of bamboo polysaccharide
(1) sulfuric acid-En ketone solution preparation: take by weighing anthrone 0.2g, vitriol oil constant volume is in the 100mL volumetric flask, and mixing gets final product, and is now with the current.
(2) preparation of standard glucose solution: precision takes by weighing the dextrose anhydrous that is dried to constant weight and is mixed with the solution that concentration is 0.1200mg/mL, and is standby.
(3) the glucose typical curve is drawn: accurately draw 0.0mL, 0.1mL, 0.2mL, 0.3mL, 0.4mL, 0.6mL, 0.8mL in 10mL tool plug test tube, supply 1.0mL with distilled water, do blank with 1.0mL distilled water, respectively add 4mL sulfuric acid-En ketone solution then, shake up, put into frozen water and cool off, be placed on and boil 10min in the boiling water, be cooled to room temperature rapidly, measure absorbance A in 620nm.
(4) sample polysaccharide replication test: the goose feather bamboo of getting the Nanjing of 4 parts of equals in quality (2g) respectively through pulverizing, the floor file bamboo, mao bamboon, Tang Zhu and spun gold cizu bottom, in 30 samples such as Chizhou City, Anhui mao bamboon any one, bamboo leaf powder places the backflow flask, extraction conditions is all solid-liquid ratio 1:30 (g:mL), 80 ℃ of temperature, extract 3h, extract twice, united extraction liquid concentrates, constant volume is got 1.0mL respectively in 10mL tool plug test tube in the 25mL volumetric flask, do blank with 1.0mL distilled water, respectively add 4mL sulfuric acid-En ketone solution then, shake up, put into frozen water and cool off, be placed on and boil 10min in the boiling water, be cooled to room temperature rapidly, measure absorbance A in 620nm.
(5) sample polysaccharide average recovery is measured: the goose feather bamboo leaf of bamboo polysaccharide extraction liquid that is equipped with the Nanjing of 0.06mg/mL, the glucose standardized solution that in the 10mL sample liquid, adds the 0.1200mg/mL of 4mL, 5mL, 6mL respectively, constant volume is got 1mL and is measured light absorption value in the 25mL volumetric flask.Each test number is done 3 points, totally 9 points.
(5) press the content that glucose standard regression equation A=5.8137C-0.00473 calculates polysaccharide in 30 kinds, screening by analysis, polysaccharide content is between 1.94%~7.69%, wherein polysaccharide content is having area, Nanjing leaflet indocalamus (4.59%) more than 4%, short indocalamus (4.82%), Bashan Mountain wood bamboo 4.43%, goose feather bamboo (7.69%), floor file bamboo (5.69%), mao bamboon (5.36%), hundred folder bamboos (4.86%), Tang Zhu (5.30%), spun gold cizu bottom (5.73%), Fujian Province Youxi green bamboo (4.36%), mao bamboon (4.72%), Chizhou City, Anhui (5.90%), especially the goose feather bamboo in Nanjing, the floor file bamboo, mao bamboon, Tang Zhu and spun gold cizu bottom, Chizhou City, Anhui mao bamboon distributes wide, polysaccharide content is higher than 5%, becomes the optimum feed stock of industrial extraction leaf of bamboo active polysaccharide component.
A kind of membrane sepn prepares the method for high purity leaf of bamboo polysaccharide,, may further comprise the steps:
The first step is extracted with the leaf of bamboo fine powder of lipophilic solvent to screening earlier, and wherein the mass ratio of lipophilic solvent and exsiccant leaf of bamboo fine powder is (1-30): 1, and for example ratio can be chosen for: 1:1,4:1,7:1,8:1,10:1,14:1,17:1,20:1,22:1,24:1,27:1,28:1,29:1,29.5:1,30:1, extracting temperature is 20 ℃-100 ℃, for example can be chosen for: 25 ℃, 35 ℃, 40 ℃, 50 ℃, 60 ℃, 70 ℃, 75 ℃, 80 ℃, 90 ℃, 98 ℃; Extraction time is 0.5h-72h, and extraction time is 0.5h, 1h, 3h, 5h, 6h, 8h, 9.5h, 12h, 14h, 15h, 16h, 17h, 18h, 20h, 30h, 35h, 40h, 55h, 60h, 70h, 71h.
In second step, use C again
1-C
3Fatty Alcohol(C12-C14 and C12-C18) or acetone remaining leaf of bamboo residue is extracted, the mass ratio of the extraction agent and the leaf of bamboo is (1-20): 1, for example ratio can be chosen for: 1:1,4:1,7:1,8:1,10:1,14:1,17:1,20:1, extracting temperature is 20 ℃-100 ℃, for example can be chosen for: 25 ℃, 35 ℃, 40 ℃, 50 ℃, 60 ℃, 70 ℃, 75 ℃, 80 ℃, 90 ℃, 98 ℃; Extraction time is 0.5h-72h; Extraction time is 0.5h, 1h, 3h, 5h, 6h, 8h, 9.5h, 12h, 14h, 15h, 16h, 17h, 18h, 20h, 30h, 35h, 40h, 55h, 60h, 70h, 71h.
The 3rd step prepared deionized water with reverse osmosis membrane purifying tap water, and with the remaining leaf of bamboo residue of deionized water extraction, the mass ratio of the deionized water and the leaf of bamboo is (1-20): 1 again,, for example ratio can be chosen for: 1:1,4:1,7:1,8:1,10:1,14:1,17:1,20:1, extracting temperature is 80 ℃-110 ℃, for example can be chosen for: 80 ℃, 85 ℃, 90 ℃, 95 ℃, 100 ℃, 105 ℃, 110 ℃; Extraction time is 0.5h-5h; For example can be chosen for 0.5h, 1h, 2h, 3h, 4h, 5h.
The 4th step, centrifugal settling: extracting solution is regulated PH to 8-9, for example 8,8.5,9, use the high speed centrifugation sedimentation, the rotating speed of whizzer is 6000-20000 rev/mins, can be chosen for 6000 rev/mins, 7000 rev/mins, 20000 rev/mins, acquisition centrifugal clear liquid and throw out; Can directly this clear liquid be carried out the film coupling in the present embodiment and separate, also can in throw out, add deionized water centrifugal settling, disgorging again, merge twice centrifugal clear liquid, wherein, the mass ratio of throw out and deionized water is 1:(1-10), can be chosen for 1:1.5,1:2,1:3,1:4,1:5,1:6,1:7,1:8,1:9
The 5th step, the film lotus root is closed separation: centrifugal clear liquid successively by ceramic membrane, ultra-filtration membrane and nanofiltration membrane treatment, is obtained the concentrated solution by nanofiltration membrane, wherein at last, the inorganic ceramic membrane material can be aluminium sesquioxide, ceramic membrane mean pore size 0.1-0.5 μ m, can for, 0.2 micron, 0.4 micron, the ultra-filtration membrane molecular weight cut-off is 5000-200000Dalton (dalton), as 5000,20000,50000,80000,100000,150000,180000,200000, nanofiltration membrane molecular weight cut-off 200-1000Dalton (dalton), material membrane flux 1-10m
3/ m
2HMPa can be chosen for 2m
3/ m
2HMPa, 3m
3/ m
2HMPa, 5m
3/ m
2HMPa, 8m
3/ m
2HMPa,
In the 6th step, decolouring is adsorbed the concentrated solution of nanofiltration membrane by decolorizing resin, and the concentrated solution volume ratio that resin adds quality and nanofiltration membrane is 1-50:100,1:100 for example, 5:100,8:100,25:100,30:100,40:100,45:100,50:100, churning time is 5-60min, for example can be chosen for 5min, 10min, 20min, 35min, 40minh, 50min, 55min, 60min, 5 ℃-80 ℃ of temperature; For example can be chosen for: 10 ℃, 15 ℃, 25 ℃, 35 ℃, 50 ℃, 55 ℃, 60 ℃, 75 ℃, 80 ℃;
In the 7th step, alcohol is analysed, and is 1.03-1.14 with the polysaccharide soln vacuum concentration after the resin decolorization to proportion, as 1.04,1.08, and 1.10,1.12,1.14; Use C
1-C
3Fatty Alcohol(C12-C14 and C12-C18) add to stir, as in methyl alcohol, the ethanol any, Fatty Alcohol(C12-C14 and C12-C18) and polysaccharide soln volume ratio are 4-20:1, for example can be chosen for 5:1,7:1,10:1,15:1,18:1,20:1; Obtain the polysaccharide precipitation thing with the filtration of 160 order filter clothes, pass through the centrifugal settling of 3000-10000r/min speed again, preferred 6000-10000r/min obtains centrifugal polysaccharide precipitation thing; The 8th step, vacuum-drying, with above-mentioned polysaccharide precipitation thing 600-2000W microwave vacuum drying, as 600W, 800W, 1200W, 1500W, 1800W, 25 ℃-60 ℃ of drying temperatures, for example, 25 ℃, 35 ℃, 50 ℃, 55 ℃, 60 ℃, vacuum tightness 250-700mmHg, for example, 250mmHg, 300mmHg, 350mmHg, 450mmHg, 550mmHg, 650mmHg, 700mmHg obtains total polysaccharides content greater than 80% leaf of bamboo polyoses extract.
In the present embodiment, the lipophilic solvent in the technical program in the first step is C
5-C
760 ℃ of-120 ℃ of sherwood oils of the fat alkane of (carbonatoms is 5-7, can be 5,6,7) or boiling range, preferred sherwood oil, normal hexane.C in second step and the 7th step
1-C
3Fatty Alcohol(C12-C14 and C12-C18) nail alcohol, ethanol, propyl alcohol, particular methanol.Decolorizing resin is D845, D941, D280, D392, D291, D730, D293, D296 etc., preferred D845, D280, D392.The leaf of bamboo of the screening in the first step, refer in particular to polysaccharide content greater than area, 4.0% Nanjing goose feather bamboo (7.69%), leaflet indocalamus (4.59%), short indocalamus (4.82%), Bashan Mountain wood bamboo (4.43%), floor file bamboo (5.69%), hundred folder bamboos (4.86%), Tang Zhu (5.30%), spun gold cizu bottom (5.73%), mao bamboon (5.36%), especially the goose feather bamboo in Nanjing, floor file bamboo, mao bamboon, Tang Zhu and spun gold cizu bottom, Chizhou City, Anhui mao bamboon distributes extensively, polysaccharide content is higher than 5%, becomes the optimum feed stock of industrial extraction leaf of bamboo active polysaccharide component.
In the technical program,, with glucose as a standard, set up analysis of polysaccharide method in the leaf of bamboo with sulfuric acid-anthrone method.Dextrose anhydrous is mixed with the solution that concentration is 0.1200mg/mL, accurately draw 0.0mL, 0.1mL, 0.2mL, 0.3mL, 0.4mL, 0.6mL, 0.8mL in 10mL tool plug test tube, supply 1mL with distilled water, do blank with 1.0mL distilled water, respectively add 4mL sulfuric acid-En ketone solution then, shake up, putting into frozen water cools off, be placed on and boil 10min in the boiling water, be cooled to room temperature rapidly, measure absorbance A in 620nm.Regression equation A=5.8137C-0.00473 (R=0.9987), glucose are the better linearity relation with absorbancy in 0.0~96.0 μ g/ml scope.
Embodiment 3
Select the fresh mao bamboon leaf 20kg of lifes in 6 years of Fujian Youxi collection in April, put the ventilating and cooling place drying, air blast 4hr below 50 ℃ in baking oven surveys water ratio and is lower than 7.0%, polysaccharide content 4.72% then.Get the 8kg dry leave, be broken into fine powder, add 60kg sherwood oil (60 ℃-90 ℃), 70 ℃ of thermal backflows are extracted, and 4 hours time, extraction for the second time adds 40kg sherwood oil (60 ℃-90 ℃), repeats above operation.United extraction liquid, 50 ℃ of following decompression and solvent recoveries.Join in the residual leaf behind the Petroleum ether extraction with the about 100L of industrial grade benzenemethanol and to extract, design temperature is 50 ℃, and lixiviate is spent the night; For the second time add 50L methanol extraction 3hr, 70 ℃ of temperature are filtered, and merge methanol extract liquid.After residual leaf dries up with open steam, add the 100L deionized water, extract 100 ℃ of temperature, extraction time 2hr filters, and repeats to extract united extraction liquid 200L 3 times.Regulate PH8.5 with the NaOH alkaline solution, naturally cool to room temperature,, obtain centrifugal clear liquid 195L with rotating speed 6000 commentaries on classics/whizzer centrifugations.Clear liquor attaches together by ceramic membrane, ultra-filtration membrane and nanofiltration membrane lotus root successively and puts processing, obtains the concentrated solution 10kg of nanofiltration membrane at last.The inorganic ceramic membrane material is an aluminium sesquioxide, and mean pore size 0.1 μ m, ultra-filtration membrane molecular weight cut-off are 100000Dalton (dalton), nanofiltration membrane molecular weight cut-off 400Dalton (dalton), material membrane flux 6m
3/ m
2HMpa.Again with the concentrated solution 10kg of nanofiltration membrane, behind 10kg D845 macroporous resin adsorption 60min, cross cleaner liquid, 80 ℃ of following vacuum concentration of temperature slowly add 95%wt ethanol 4L to proportion 1.12, stir precipitation, with rotating speed 6000 commentaries on classics/whizzer centrifugations, obtain with throw out the solid part microwave vacuum drying, 45 ℃ of temperature, vacuum tightness 700mmHg,, obtain white powder 224g, promptly be rich in high purity leaf of bamboo polyoses extract, polysaccharide 80.6%wt wherein, weight loss on drying≤5.0%wt, ash content≤3.0%wt, heavy metal≤10mg/kg, arsenic≤2mg/kg.
Embodiment 4
5 years living fresh goose mao bamboon leaf 25kg that select Nanjing Forestry University to collect October are put the ventilating and cooling place drying, and air blast 3hr below 50 ℃ in baking oven surveys water ratio and is lower than 7.0%, polysaccharide content 7.69% then.Get the 10kg dry leave, be broken into fine powder, add the 100kg normal hexane, 70 ℃ of thermal backflows are extracted, and 2 hours time, extraction for the second time adds the 50kg normal hexane, repeats above operation.United extraction liquid, 50 ℃ of following decompression and solvent recoveries.Join in the residual leaf after normal hexane extracts with technical grade ethanol 100L and to extract, design temperature is 70 ℃, time 2hu; For the second time add 50L extraction using alcohol 3hr, 70 ℃ of temperature are filtered, and merge ethanol extract.After residual leaf dries up with open steam, add the 150L deionized water, extract 100 ℃ of temperature, extraction time 3hr filters, and repeats to extract united extraction liquid 250L 3 times.Regulate PH8.5 with the NaOH alkaline solution, naturally cool to room temperature,, obtain centrifugal clear liquid 240L with rotating speed 6000 commentaries on classics/whizzer centrifugations.Clear liquor attaches together by ceramic membrane, ultra-filtration membrane and nanofiltration membrane lotus root successively and puts processing, obtains the concentrated solution 10kg of nanofiltration membrane at last.The inorganic ceramic membrane material is an aluminium sesquioxide, and mean pore size 0.4 μ m, ultra-filtration membrane molecular weight cut-off are 150000Dalton (dalton), nanofiltration membrane molecular weight cut-off 300Dalton (dalton), material membrane flux 6m
3/ m
2HMpa.With the concentrated solution 10kg of nanofiltration membrane, behind 8kg D280 macroporous resin adsorption 40min, cross cleaner liquid again, 80 ℃ of following vacuum concentration of temperature slowly add 95% ethanol 5L to proportion 1.10, stir precipitation, with rotating speed 6000 commentaries on classics/whizzer centrifugations, obtain with throw out the solid part microwave vacuum drying, 50 ℃ of temperature, vacuum tightness 700mmHg,, obtain white powder 540g, promptly be rich in high purity leaf of bamboo polyoses extract, wherein polysaccharide 88.7%wt.
The 8 years fresh spun gold cizu of life bottom leaf 25kg that select Nanjing Forestry University to collect October are put the ventilating and cooling place drying, and air blast 3hr below 50 ℃ in baking oven surveys water ratio and is lower than 7.0%wt, polysaccharide content 5.73% then.Get the 10kg dry leave, be broken into fine powder, the extraction and separation method of polysaccharide is identical with embodiment 4, and the macropore decolorizing resin adopts D392, obtains white powder 260g, promptly is rich in high purity leaf of bamboo polyoses extract, wherein polysaccharide 82.1%wt.
Embodiment 6
The fresh mao bamboon leaf 20kg of lifes in 15 years that selects the little Chizhou City of peace to collect March is put the ventilating and cooling place drying, and air blast 5hr below 50 ℃ in baking oven surveys water ratio and is lower than 7.0%, polysaccharide content 5.90% then.Get the 10kg dry leave, be broken into fine powder, the extraction and separation method of polysaccharide is identical with embodiment 3, and the macropore decolorizing resin adopts D293, obtains white powder 249g, promptly is rich in high purity leaf of bamboo polyoses extract, and wherein polysaccharide 81.4%.
Embodiment 7
The fresh floor file leaf of bamboo 20kg of lifes in 8 years that selects Nanjing Forestry University to collect October is put the ventilating and cooling place drying, and air blast 5hr below 50 ℃ in baking oven surveys water ratio and is lower than 7.0%, polysaccharide content 5.69% then.Get the 10kg dry leave, be broken into fine powder, the extraction and separation method of polysaccharide is identical with embodiment 4, and the macropore decolorizing resin adopts D296, obtains white powder 220g, promptly is rich in high purity leaf of bamboo polyoses extract, wherein polysaccharide 80.2%wt.
Embodiment 8
8 years fresh indicalamus leaf 20kg of life that select Nanjing Forestry University to collect October are put the ventilating and cooling place drying, and air blast 5hr below 50 ℃ in baking oven surveys water ratio and is lower than 7.0%, polysaccharide content 2.66% then.Get the 10kg dry leave, be broken into fine powder, add the 150L deionized water, extract 100 ℃ of temperature, extraction time 2hr filters, and repeats to extract united extraction liquid 250L 3 times.Clear liquor attaches together by ceramic membrane, ultra-filtration membrane and nanofiltration membrane lotus root successively and puts processing, obtains the concentrated solution 10kg of nanofiltration membrane at last.The inorganic ceramic membrane material is an aluminium sesquioxide, and mean pore size 0.5 μ m, ultra-filtration membrane molecular weight cut-off are 80000Dalton (dalton), nanofiltration membrane molecular weight cut-off 500Dalton (dalton), material membrane flux 6m
3/ m
2HMpa.With the concentrated solution 10kg of nanofiltration membrane, behind 8kg D280 macroporous resin adsorption 60min, cross cleaner liquid again, 80 ℃ of following vacuum concentration of temperature slowly add 95% ethanol 5L to proportion 1.10, stir precipitation, with rotating speed 6000 commentaries on classics/whizzer centrifugations, obtain with throw out the solid part microwave vacuum drying, 60 ℃ of temperature, vacuum tightness 700mmHg,, obtain white powder 345g, promptly be rich in high purity leaf of bamboo polyoses extract, wherein polysaccharide 48.3%wt.
Claims (7)
1. the method for a preparing bamboo leaf polysaccharide extract by member separation is characterized in that may further comprise the steps:
The first step is extracted the leaf of bamboo polysaccharide content that the filters out leaf of bamboo greater than 5.0%wt with lipophilic solvent earlier, and wherein the mass ratio of lipophilic solvent and the leaf of bamboo is (1-30): 1, and the extraction temperature is 20 ℃-100 ℃, extraction time is 0.5h-72h; Wherein, leaf of bamboo polysaccharide content greater than the screening method of the leaf of bamboo of 5.0%wt is: with sulfuric acid-anthrone method, with glucose as a standard, set up the glucose typical curve, product with glucose as a standard then, under the 610nm leaf of bamboo of collecting is carried out colorimetric estimation leaf of bamboo polysaccharide content, filter out the leaf of bamboo of leaf of bamboo polysaccharide content greater than 5.0%wt;
In second step, use C again
1-C
3Fatty Alcohol(C12-C14 and C12-C18) or acetone to be extraction agent extract the leaf of bamboo residue of the first step, the mass ratio of the extraction agent and the leaf of bamboo is (1-20): 1, extracting temperature is 20 ℃-100 ℃, extraction time is 0.5h-72h;
In the 3rd step, with the leaf of bamboo residue that second step of deionized water extraction obtains, the mass ratio of the deionized water and the leaf of bamboo is (1-20): 1, and extracting temperature is 80 ℃-110 ℃, extraction time is 0.5h-5h;
The 4th step, centrifugal settling: the extracting solution that the 3rd step obtained is regulated pH to 8-9,, obtain centrifugal clear liquid and throw out with the centrifugal settling of 6000-20000r/min speed;
The 5th step, the film lotus root is closed separation: the centrifugal clear liquid that the 4th step was obtained obtains concentrated solution at last by ceramic membrane, ultra-filtration membrane and nanofiltration membrane treatment successively, wherein, the ceramic membrane mean pore size is 0.1-0.5 μ m, the ultra-filtration membrane molecular weight cut-off is 5000-200000 dalton, nanofiltration membrane molecular weight cut-off 200-1000 dalton, material is by ultra-filtration membrane and nanofiltration membrane flux 1-10m
3/ m
2HMPa;
The 6th step, decolouring, the concentrated solution that the 5th step was obtained adsorbs by decolorizing resin, and the ratio of the volume of the quality of the resin of adding and the concentrated solution of adding is 1-50: 100, churning time is 5-60min, 5 ℃-80 ℃ of temperature;
In the 7th step, alcohol is analysed, and the 6th leaf of bamboo polysaccharide soln of step after the resin decolorization is vacuumized to be concentrated into proportion be 1.03-1.14, adds C
1-C
3Fatty Alcohol(C12-C14 and C12-C18) stir, Fatty Alcohol(C12-C14 and C12-C18) and polysaccharide soln volume ratio are 4-20: 1, obtain throw out with the filtration of 160 order filter clothes again;
The 8th step, vacuum-drying, the throw out that the 7th step obtained is centrifugal, solid part 600-2000W microwave vacuum drying, 25 ℃-60 ℃ of temperature, vacuum tightness 250-700mmHg obtains the leaf of bamboo polyoses extract of leaf of bamboo polysaccharide content greater than 80%wt.
2. the method for preparing bamboo leaf polysaccharide extract by member separation according to claim 1 is characterized in that the leaf of bamboo in the first step, refers in particular to the leaf of bamboo of goose feather bamboo, floor file bamboo, mao bamboon, Tang Zhu or the spun gold cizu bottom in Nanjing, perhaps the leaf of bamboo of Chizhou City, Anhui mao bamboon.
3. the method for preparing bamboo leaf polysaccharide extract by member separation according to claim 1 is characterized in that described C
1-C
3Fatty Alcohol(C12-C14 and C12-C18) be in methyl alcohol, ethanol, the n-propyl alcohol any one.
4. the method for preparing bamboo leaf polysaccharide extract by member separation according to claim 1 is characterized in that lipophilic solvent is C in the first step
5-C
7Fat alkane or the boiling range sherwood oil that is 60 ℃-120 ℃.
5. the method for preparing bamboo leaf polysaccharide extract by member separation according to claim 4 is characterized in that described C
5-C
7Fat alkane be in Skellysolve A, normal hexane or the normal heptane any one.
6. the method for preparing bamboo leaf polysaccharide extract by member separation according to claim 1 is characterized in that decolorizing resin in the 6th step, refers among D845, D941, D280, D392, D291, D730, D293, the D296 any one.
7. the method for preparing bamboo leaf polysaccharide extract by member separation according to claim 1 is characterized in that extracting mode in the first step can select any one or the combination in thermal backflow extraction, microwave extraction, the ultrasonic extraction.
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CN104017095B (en) * | 2013-03-01 | 2016-08-17 | 浙江大学 | The extraction method of bamboo polysaccharide |
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CN109734821A (en) * | 2018-12-20 | 2019-05-10 | 广西中医药大学 | A kind of extracting method of natural bambo juice polysaccharide |
CN110092847A (en) * | 2019-06-13 | 2019-08-06 | 江南大学 | A method of extracting Polysaccharides in Bamboo Leaves |
CN110256589A (en) * | 2019-06-15 | 2019-09-20 | 浙江科技学院 | A kind of method that ultrasonic wave-coupled heteropoly acid technology for hydrolyzing extracts Polysaccharides in Bamboo Leaves |
CN110256597B (en) * | 2019-07-12 | 2021-09-24 | 华茂(湖州)保健品有限公司 | Method for reducing heavy metal residues in ganoderma lucidum polysaccharide by membrane method |
CN110396137A (en) * | 2019-08-28 | 2019-11-01 | 四川丰泰食品科技有限公司 | A method of extracting Polysaccharides in Bamboo Leaves |
CN115340614A (en) * | 2022-10-06 | 2022-11-15 | 吉林农业大学 | Method for decoloring ginseng residue polysaccharide by using ultrasonic-assisted macroporous resin |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5589591A (en) * | 1986-07-03 | 1996-12-31 | Advanced Magnetics, Inc. | Endotoxin-free polysaccharides |
CN1546532A (en) * | 2003-11-28 | 2004-11-17 | 河北农业大学 | Method for extracting and purifying lipopolysaccharide from corn soaking water |
-
2008
- 2008-11-05 CN CN2008101950631A patent/CN101392032B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5589591A (en) * | 1986-07-03 | 1996-12-31 | Advanced Magnetics, Inc. | Endotoxin-free polysaccharides |
CN1546532A (en) * | 2003-11-28 | 2004-11-17 | 河北农业大学 | Method for extracting and purifying lipopolysaccharide from corn soaking water |
Non-Patent Citations (5)
Title |
---|
JP特开平10-120704A 1998.05.12 |
丁红秀.毛竹叶多糖构成及生物活性研究.《中国博士学位论文全文数据库 医药卫生科技辑》.2008,(第7期),第21-23,26页. * |
叶建中等.高品质竹叶多糖的筛选及含量测定方法的研究.《现代化工》.2008,第28卷第268-270页. * |
李胜华等.竹叶多糖的提取工艺.《吉首大学学报(自然科学版)》.2006,第27卷(第1期),第118-121页. * |
郑渊月.毛竹叶活性多糖、类黄酮的中试提取及分离纯化研究.《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》.2006,(第10期),32-35页. * |
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